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Z <br />established the sizes of the motors that are connected with the a111liAg nrachiu- <br />ery. Laboratory experiments, pilot teats, and practical experience were also <br />• factored into the choice of this flow sheet, which resulted in the final mill deer <br />Ore from C.O.M. Int.'s mines ' transported to the millsite in a dum ck, and ~ re-- <br />ore bins. 'These ore bins feed the crushing ~~ <br />plant, which incorporates primary and secondary crushers in a closed-circuit. ~ ~° r - <br />After crushing, the ore is stored in a fine ore bin with enough capacity tq insure <br />~ an 8 hour supply of ore for the grinding and concentrating cirouita of the mill. <br />This fine ore is then conveyed to the grinding circuit to complete the comminu- <br />tion process. Fresh water is added to the ore for wet grinding in a ball mill that <br />is in closed-circuit with a spiral classifier. Gravity concentration follows the <br />grinding circuit, with separation being accomplished by a double jig, a rag plant, <br />and a shaking table. The gravity concentrates from each machine in this eec- <br />• tion of the plant is pulled fi»m the milling circuit for collection and further <br />treataent. The overflow from the shaking table carries the suspended, finely <br />divided fraction of the pulverized ore to a large thickener tank. This thickener <br />tank serves two important functions. It clarifies the mill water, which ie re- <br />turned to the ball mill for recycline in the gravity circuit, and it increases the <br />• concentration of the suspended solids prior to their flotation. The clarified <br />water overflows a peripheral launder, while the solids settle on the bottom of <br />the tank Four rotating radial arms with blades rake the settled solids towards <br />an outlet at the center of the bottom of the tank. These rotating blades also <br />assist in the compaction of'the settled particles, produce a thicker underfloor, <br />and promote faster clarification of the mill water. A diaphragm pump is used <br />• to lift the thickened pulp to a bank of flotation cells, where the concentration <br />process is completed. Standard flotation reagents such as pine oil, soda ash, <br />and santhate are used in the flotation cells. 'The tailings from the flotation <br />circuit are pumped to the tailings pond, and the final concentrate pulp is col- <br />lected for filtration. A disc vacuum filter dewatere the flotation concentrate, <br />• which is shipped from the millsite for further treatment. <br />C.O.M. Iuc.'s designed to have th bility prooe~0 tone of o <br />a our peri ecauee the crushing p nt eectron of the re a e to <br />true enoug ore in a single 8-hour shift to furnish the grinding circuit of the <br />mill with a 24-hour supply of fine ore, it will only be operated one shift a day. In <br />• order to achieve efficient grinding, maintain the ratio of concentration, and in- <br />sure ahigh level of recovery, the grinding and concentrating circuits will be <br />operated continuously. Initially, the milling facility will be operated 3 or 4 days <br />a week for 24 hours a day. This schedule is based upon pralucing 50 tons of <br />ore a day from C.O.M. Ines properties. <br />• Tailings Impoundment Area <br />On August 28, 1994, the site was visited by representatives from Mine Safety <br />and Health Administration at C.O.M., Int.'s request. ?here were satisfied that <br />the tailings impoundment was installed correctly, a Dopy of their opinion will be <br />• f'orwanded to division under a separate cover. ~ ~. ~~~~~_ ~~ <br />Ji a+~ <br />~. <br />'~`;, ~ ~~ <br />~. <br />